Milk-based alternative product and method for producing the same

ABSTRACT

The present invention concerns the production of a milk-based alternative product, using edible oil to substitute at least part of the milk fat. In particular, the present invention concerns the production of a cheese alternative product, an ice cream alternative product, a custard alternative product or a chilled or frozen dessert alternative product, using an edible oil to substitute at least part of the milk fat. Further, a milk based alternative product, in particular a cheese alternative product, an ice cream alternative product, a custard alternative product or a chilled or frozen dessert alternative product, and the use of an edible oil, in particular olive oil, for the production of the milk-based alternative product are disclosed.

RELATED APPLICATIONS

This application is a continuation application of U.S. patentapplication Ser. No. 13/202,562, filed on Aug. 19, 2011, now abandoned,which, in turn, is the U.S. National Stage of International ApplicationSerial No.: PCT/EP2010/069282, filed Dec. 9, 2010, which claims thebenefit of European Application No. 0938603.9, filed on Dec. 11, 2009.The entire teachings of the above applications are incorporated hereinby reference.

FIELD OF THE INVENTION

The present invention concerns the production of a milk-basedalternative product, using edible oil to substitute at least part of themilk fat. In particular, the present invention concerns the productionof a cheese alternative product, an ice cream alternative product, acustard alternative product or a chilled or frozen dessert alternativeproduct, using an edible oil to substitute at least part of the milkfat.

Further, a milk-based alternative product, in particular a cheesealternative product, an ice cream alternative product, a custardalternative product or a chilled or frozen dessert alternative productand the use of an edible oil, in particular olive oil, for theproduction of the milk-based alternative product are disclosed.

BACKGROUND OF THE INVENTION

Nowadays, the consumer preferences have been oriented towards morehealthy eating habits. Milk-based products, such as cheese may be ahigh-fat source, but also an excellent source of calcium and protein.The practice to reduce fat content in cheeses has often been correlatedwith reduced taste, flavor and texture in the resulting fat-reducedproducts.

Examples of vegetable-fat based cheese alternative products may be foundin the literature, the majority concerning processed cheesemanufacturing methods. Fewer attempts have been made to produce cheeseproducts designed to resemble natural/traditional cheeses. To achievethe desirable stability of vegetable oil incorporation in the dairyproduct, most approaches adopted, include the use of efficientemulsifying agents and adequate amounts thereof.

EP 0 368 492 teaches a method for preparing a cheese product having alow level of saturated fat and cholesterol. The invention makes use of avegetable fat-based cream added to skim, semi-skimmed or low fat milk,adding to a cheese vat and processing using conventional techniques toform cheese. The said vegetable fat-based cream is prepared by adding ablend of vegetable pasteurized oils, such as soya oil and hydrogenatedsoya oil and an emulsifier to an aqueous phase comprising a pasteurizedblend of water and a stabilizer, such as gelatin. In one embodiment ofthe invention the vegetable fat comprises a blend of vegetable fats,which has a similar melting point profile to milk fat over the range of5° C. to 38° C.

Another example of a low cholesterol dairy product may be produced,according to U.S. Pat. No. 5,063,074. Its disclosure relates to thecombination of skim milk with a pre-mix comprising a vegetable oilcarrier as well as agents, which impart texture and flavoring propertiesto the milk product. The resultant fluid milk can be pasteurized andstored at refrigerated temperatures for at least six weeks, until it isused to produce a number of dairy products, including hard cheese. Inrepresentative formulations, which are disclosed in U.S. Pat. No.5,063,074, the premix is comprised of vegetable oil, emulsifiers, gumsand flavoring agents.

Cheese alternatives having incorporated natural vegetable oils aresusceptible to oil exudation phenomena and they are often unacceptablein texture due to reduced firmness. The presence of vegetable oil inpartial substitution of dairy fat may affect the process called“syneresis”, the process referring to curd and whey separation.Sometimes, the vegetable oil may prevent the necessary expulsion ofwhey.

The present invention has the object to overcome the disadvantages ofthe prior art. In particular, the invention aims to provide a cheap,easy to use process for the production of a milk-based alternativeproduct, such as a cheese alternative product, an ice cream alternativeproduct, a custard alternative product or a chilled or frozen dessertalternative product. The process shall be as close to thenatural/traditional process for the production of the particularmilk-based product, i.e. cheese, ice cream, custard, chilled or frozendesert, as possible. In particular, it is not desired to de-fat thebasic milk but rather to substitute at least part of the milk fat by anedible oil.

SUMMARY OF THE INVENTION

The present invention provides a method for producing a cheesealternative product comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) subjecting the mixture to a curd formation,    -   h) performing a curd and whey separation,        wherein a cheese alternative product is obtained, which contains        5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat, more        preferably about 5 to 25 (w/w) % fat and most preferably about 5        to 20 (w/w) % fat.

The invention further comprises a cheese alternative product, obtainableby a method comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55 20 C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) subjecting the mixture to a curd formation,    -   h) performing a curd and whey separation,        wherein a cheese alternative product is obtained, which contains        5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat, more        preferably about 5 to 25 (w/w) % fat and most preferably about 5        to 20 (w/w) % fat.

Further, the invention discloses the use of an edible oil for theproduction of a cheese alternative product, wherein the cheesealternative product contains 5 (w/w) % fat, preferably about 5 to 30(w/w) % fat, more preferably about 5 to 25 (w/w) % fat and even morepreferably about 5 to 20 (w/w) %.

Moreover, the invention comprises a method for producing a milk-basedalternative product, in particular an ice cream alternative product, acustard alternative product or a chilled or frozen dessert alternativeproduct, comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) further processing of the pasteurized mixture in order to        obtain a milk- based product, such as an ice cream, a custard, a        chilled or frozen dessert, using appropriate methodologies known        in the art suited for each product type,        wherein a milk-based alternative product is obtained, which        contains 5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat,        more preferably about 5 to 25 (w/w) % fat and most preferably        about 5 to 20 (w/w) % fat.

The invention further comprises a milk-based alternative product, inparticular an ice cream alternative product, a custard alternativeproduct or a chilled or frozen dessert alternative product, obtainableby a method comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) further processing of the pasteurized mixture in order to        obtain a milk- based product, such as an ice cream, a custard, a        chilled or frozen dessert, using appropriate methodologies known        in the art suited for each product type,        wherein a milk-based alternative product is obtained, which        contains 5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat,        more preferably about 5 to 25 (w/w) % fat and most preferably        about 5 to 20 (w/w) % fat.

Further, the invention discloses the use of an edible oil for theproduction of a milk-based alternative product, in particular an icecream alternative product, a custard alternative product or a chilled orfrozen desert alternative product, wherein the milk-based alternativeproduct contains 5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat,more preferably about 5 to 25 (w/w) % fat and even more preferably about5 to 20 (w/w) % fat.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 shows a flow diagram of the inventive process. Specifically, FIG.1 shows the production of vegetable oil-containing milk based products.

DETAILED DESCRIPTION OF THE INVENTION

The present invention relates to emulsion-type foodstuff in general and,in particular, to milk-based alternative products, such as cheesealternative products, ice cream alternative products, custardalternative products or chilled or frozen dessert alternative products,made by incorporating vegetable oil into skimmed milk and furtherprocessing the resulting mixture under selective conditions, to form amilk-based alternative product having the desired texture and flavor.

In particular, the inventors provide a method for producing a cheesealternative product comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) subjecting the mixture to a curd formation,    -   h) performing a curd and whey separation,        wherein a cheese alternative product is obtained, which contains        5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat, more        preferably about 5 to 25 (w/w) % fat and most preferably about 5        to 20 (w/w) % fat.

In a particular preferred embodiment, the milk is whole milk,semi-skimmed milk or skimmed milk, preferably skimmed milk.

An edible oil, in particular a vegetable oil-containing alternativecheese is produced by removing the milk fat from the milk, theninserting therein an amount of vegetable oil, homogenizing the resultingmixture and subjecting said vegetable oil-containing milk into selectivecheese processing conditions. The resulting alternative cheese may befurther used to produce processed type cheeses.

The present invention provides cheese product alternatives/analoguesresembling the related natural/traditional cheese products. The cheesealternative products are prepared by homogenizing a vegetable fat into askimmed or semi-skimmed milk and further processing the oil-containingmilk, using conditions favoring syneresis.

The stable incorporation of vegetable oil in the cheese product, isherein assured by:

-   -   i) The oil insertion system that introduces the oil into the        milk flow at conditions allowing the dispersion of oil globules        in the milk carrier. Using the herein described oil insertion        system, mild homogenization conditions may be applied, favoring        syneresis and promoting whey separation. Intense homogenization,        on the other hand, may dramatically increase the amount of oil        globules. This means, that a greater amount of available casein        proteins should become adsorbed onto the surface of oil        globules, a phenomenon that destabilizes the curd, by reducing        syneresis and delaying whey separation. Thus, a mild        homogenization procedure is preferred.    -   ii) The selective cheese making conditions, optimized to ensure        consistently stable organoleptic features.

The vegetable oil is subjected to mild heating, until a temperature ofabout 50-55° C. has been reached. Then, the vegetable oil is insertedinto the skimmed milk. The skimmed milk forms the carrier in thecontinuous flow system, wherein the oil is inserted. In a flow diagram,the oil insertion system is situated immediately after the milk creamseparator. The skimmed milk passes at a pressure of approximately 2.3bars and a flow rate at about 10 tons/hour-12 tons/hour. The vegetableoil insertion system comprises a 30-40 mm diameter tube, along which thevegetable oil is passed at a pressure of 2.5 bars and a flow rate ofapproximately 500-2000 liters per hour, preferably at >or =1000 litersper hour, more preferably at >or =1500 liters per hour and even morepreferably at 2000 liters per hour, depending on the intended oil/milkmixing ratio at the time of insertion. Next, the oil-containing milk isdirected to a homogenizer, whereby the oil droplets are reduced in sizeand homogenously dispersed in milk, following a mild homogenization at10 bar. Then, the resulting oil-containing milk is held at 72°°C. for 15sec, cooled down to 4-6° C. and stored. Curd formation follows, undersuitable conditions (as shown in the Examples), by the addition ofsuitable amounts of rennet and/or microbial starter cultures. Finallycurd-whey separation procedure follows, using optimized conditions,suited for each product type, as described in the Examples. Optionally,the resulting cheese alternative products are used for the making ofprocessed type cheeses, according to the common methods known in theart.

Within the context of the present invention, the term “oil”, wheneverused herein, comprises any edible oil fit for human consumption ormixtures thereof. Preferably, the oil is a vegetable oil. Some of themany different kinds of edible vegetable oils, that can be used, includeolive oil, palm oil, soybean oil, canola oil, pumpkin seed oil, cornoil, rape oil, sunflower oil, safflower oil, peanut oil, walnut oil,wheat germ oil, grape seed oil, sesame oil, argan oil, rice bran oil andmixtures thereof. Many other kinds of vegetable oils that are used forcooking can, however, also be used according to the present application.From the oils mentioned above, olive oil, sunflower oil, corn oil, rapeoil and mixtures thereof are especially preferred, with olive oil beingthe most preferred oil. Especially preferred, the oil is virgin oliveoil or extra virgin olive oil. Moreover, it is also preferred that theoil used according to the present application is an organic oil.

The milk used for the preparation of the cheese may be whole milk orpartially or wholly skimmed milk. The vegetable oil may be used at leastin partial substitution of milk fat. Milk can be of cow, goat, sheep orbuffalo origin, or any combination thereof.

The use of stabilising agents or/and emulsifying agents is possible, butnot compulsory.

In a preferred embodiment, inserting the oil in step c) is performed byan insertion tube with a diameter of about 32 mm.

In a further preferred embodiment the flow rate of the edible oil instep c) is about 1000 to 2000 liters/h, preferably 1000 liters/h, morepreferably 1500 liters/h and most preferably about 2000 liters/h.

In another embodiment the homogenization in step d) uses a two-stagehomogenizer with a piston diameter of about 55 mm.

The amount of the oil that is to be used for the preparation of theoil-containing milk-based products particularly depends on the kind ofoil, the kind of milk and the intended oil end concentration of thecheese alternative products to be prepared. An exemplary amount of theoil concentration of the mixture in step f) is between about 4 to 17(w/w) %, more preferably about 8 to 17 (w/w) % and even more preferablyabout 9 to 17 (w/w) %.

The resulting product of the present invention may be a cheesealternative product from the list of cheese alternatives, including:semi-hard cheese type (such as, semi-hard pasta fillata type, etc.),hard cheese type, white cheese in brine, whey cheese type, soft cheesetype, surface ripened cheese type, blue veined cheese type andspreadable cheese type.

According to the present invention, the oil-containing milk-basedproduct contains the oil as a substitute for the milk fat content. Thecheese alternative product may, however, also contain both vegetable oiland milk fat.

A further object of the present invention is a cheese alternativeproduct, obtainable by a method comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) subjecting the mixture to a curd formation,    -   h) performing a curd and whey separation,        wherein a cheese alternative product is obtained, which contains        5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat, more        preferably about 5 to 25 (w/w) % fat and most preferably about 5        to 20 (w/w) % fat.

In a preferred embodiment the curd formation and the curd and wheyseparation are performed by:

-   -   i) inoculating the pasteurized mixture with suitable amounts of        a mesophilic and/or thermophilic and/or propionic acid starter        culture and/or rennet to coagulate the mixture,    -   j) subjecting the curd to syneresis favoring conditions to        separate the curd from the whey.

The invention further encompasses a semi-hard cheese alternative productobtainable by the inventive process, wherein:

-   -   the mixture comprises a fat/protein ratio of 0.4 to 0.9,    -   the mixture is heated up to the temperature of 34 to 36° C.,    -   the rennet comprises a composition of 90% chymosin and 10%        pepsin,    -   the coagulation is accomplished at 34 to 36° C. for 35 to 45        min,    -   cutting the curd into up to 2 to 5 mm grains, stirring the        grains for 12 min at a gradually increasing temperature to reach        42° C., further stirring the grains for 15 min at a gradually        increasing temperature to reach 51° C. and further stirring at a        steady temperature of 51° C. for <45 min,    -   in a preferred embodiment, the curd has a final pH of about 6.2        to 6.25.    -   the curd is pressed at 80 to 100 psi for 40 min before        subjecting to traditional cheese aging.

The invention further encompasses another type of a semi-hard cheesealternative product, obtainable by the inventive process, wherein:

-   -   the mixture comprises a fat/protein ratio of 0.4 to 0.5,    -   the mixture is heated up to the temperature of 31 to 32° C.,    -   the rennet comprises a composition of 90% chymosin and 10%        pepsin,    -   the coagulation is accomplished at 31 to 32° C. for 35 to 45        min,    -   cutting the curd into up to 2 to 5 mm grains, draining off about        40 (w/w) % of whey, adding 35 (w/w) % amount of water of a        temperature of 36° C., heating and stirring the grains at 34° C.        for 40 min,    -   in a preferred embodiment, the curd has a final pH of about        5.4-5.6,    -   the curd is pressed at 80 to 100 psi for 40 min before        subjecting to natural/traditional cheese aging.

Additionally, a hard cheese alternative product is obtainable, in which:

-   -   the mixture comprises a fat/protein ratio of 1.0 to 1.1,    -   the mixture is heated up to the temperature of 34 to 36° C.,    -   the rennet comprises a composition of 90% chymosin and 10%        pepsin,    -   the coagulation is accomplished at 34 to 36° C. for 35 min,    -   cutting the curd into up to 5 to 8 mm grains, heating and        stirring the curd grains up to 46° C., replacing 20% of the whey        with water of a temperature of 45° C., continue stirring the        grains for up to about 48° C. and resting the curd at about        48° C. for 10 min, and    -   the curd is pressed at 80 to 100 psi before subjecting to        natural/traditional cheese aging,    -   in a preferred embodiment the curd has a final pH of about 5.3        to 5.4.

Further disclosed is a brine cheese alternative, obtainable by theinventive process, wherein:

-   -   the mixture comprises a fat/protein ratio of 0.4 to 0.9,    -   the mixture is heated up to the temperature of 38° C.,    -   the pasteurized mixture is inoculated with a suitable bulk        starter culture and rennet of 90% chymosin and 10% pepsin,    -   the coagulation is accomplished at 38° C. for about 50 min,    -   cutting the curd into 1 cm×1 cm×2 cm to 2 cm×2 cm×2 cm grains        and resting the curd for 65 min, and    -   the curd is transferred to molds and whey drainage occurs due to        gravity.

Further disclosed is the use of an edible oil for the production of acheese alternative product, wherein the cheese alternative productcontains 5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat, morepreferably about 5 to 25 (w/w) % fat and most preferably about 5 to 20(w/w) % fat.

Moreover, the inventors provide a method for producing a milk-basedalternative product, in particular an ice cream alternative product, acustard alternative product or a chilled or frozen dessert alternativeproduct, comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) further processing of the pasteurized mixture in order to        obtain a milk- based product, such as an ice cream, a custard, a        chilled or frozen dessert, using appropriate methodologies known        in the art suited for each product type,        wherein a milk-based alternative product is obtained, which        contains 5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat,        more preferably about 5 to 25 (w/w) % fat and most preferably        about 5 to 20 (w/w) % fat.

In a particular preferred embodiment, the milk is whole milk,semi-skimmed milk or skimmed milk, preferably skimmed milk.

An edible oil (in particular vegetable oil)-containing milk-basedalternative product is produced by removing the milk fat from the milk,then inserting therein an amount of vegetable oil, as in the steps (a)to (c), homogenizing the resulting mixture, as in step (d) andsubjecting said vegetable oil-containing milk to milk-based productprocessing conditions. The resulting milk-based alternative product maybe further used to produce successive products.

The present invention provides milk-based product alternatives/analoguesresembling the related natural/traditional milk-based products. Themilk-based alternative products, such as ice cream alternative products,custard alternative products or chilled or frozen dessert alternativeproducts, are prepared by inserting an amount of vegetable fat into askimmed or semi-skimmed milk, as aforementioned, subjecting theresulting mixture to mild homogenization and further processing theresulting oil-containing milk according to methods known in the art forthe making of ice cream, custards, or chilled or frozen desserts.

For example, for the making of an alternative ice-cream product, thevegetable oil is first subjected to mild heating, until a temperature ofabout 50-55° C. has been reached. Then, the vegetable oil is inserted inthe skimmed milk. The skimmed milk forms the carrier in the continuousflow system, wherein the oil is inserted. In a flow diagram, the oilinsertion system is situated immediately after the milk cream separator.The skimmed milk passes at a pressure of approximately 2.3 bars and aflow rate at about 10 tons/hour to 12 tons/hour. The vegetable oilinsertion system comprises a 30-40 mm diameter tube, along which thevegetable oil is passed at a pressure of 2.5 bars and a flow rate ofapproximately 500-2000 liters/hour, preferably at 1000 litres/ hour,more preferably at 1500 litres/hour and even more preferably at 2000litres/hour, depending on the intended oil/milk mixing ratio at the timeof insertion. Next, the oil-containing milk is directed to ahomogenizer, whereby the oil droplets are reduced in size andhomogenously dispersed in the milk, following a mild homogenization at10 bar. Then, the resulting oil-containing milk is held at 72° C. for 15sec, cooled down to 4-6° C. and stored. Following cooling, a primaryingredient or a mixture thereof is added and mixed therein. The primaryingredient is preferably selected from the group comprising sweeteners,stabilizers and thickeners. Examples of sweeteners include sucrose,fructose, glucose, aspartame, sorbitol, etc. Appropriate stabilizers andthickeners include, for example, carrageenan, sodium alginate, etc. Theprocedure follows with the admixture of a secondary ingredient or amixture thereof. The secondary ingredient for the making of ice-cream ispreferably selected from the group comprising fat or a fat containingingredient/composition, such as milk cream, milk fat, vegetable fat oroil, and emulsifiers, such as egg yolk, lecithin, glycerinemonostearate, PGPR, tweens, etc. The quantities of the primary andsecondary ingredients used are in accordance with supplierspecifications and regulation. For all the added ingredients to beproperly dissolved, the resulting mixture is then subjected to a heattreatment up to 68° C. Following this heat treatment, the mixture ishomogenized at about 100 bar and up to 200 bar and pasteurized at 78-80°C. for 20-25 sec. The pasteurized oil containing-milk mixture is cooledto approximately 5° C. and incubated for at least 4 hours at the sametemperature for “aging”. Following aging, the mixture is subjected tofreezing and whipping (“churning”), for the size of fat crystals to bereduced and sufficient air to be incorporated in the mass of themixture. The addition of aromas (i.e. artificial and/or natural foodgrade, such as vanillin, strawberry extracts, etc.) and colourings (i.e.artificial and/or natural food grade, such as cochineal, beta-carotene,annatto, etc.) and optionally garniture (such as chocolate chips, nuts,etc) may be done in this step. Finally, the resulting mixture is filledin appropriate containers and is subjected to further freezing (e.g.blast freezer conditions: −40° C.), before storage at −20° C.

For example, for the making of an alternative custard, the vegetable oilis first subjected to mild heating, until a temperature of about 50-55°C. has been reached. Then, the vegetable oil is inserted in the skimmedmilk. The skimmed milk forms the carrier in the continuous flow system,wherein the oil is inserted. In a flow diagram, the oil insertion systemis situated immediately after the milk cream separator. The skimmed milkpasses at a pressure of approximately 2.3 bars and a flow rate at about10 tons/hour to 12 tons/hour. The vegetable oil insertion systemcomprises a 30-40 mm diameter tube, along which the vegetable oil ispassed at a pressure of 2.5 bars and a flow rate of approximately500-2000 litres/hour, preferably at 1000 litres/hour, more preferably at1500 litres/hour and even more preferably at 2000 litres/hour, dependingon the intended oil/milk mixing ratio at the time of insertion. Next,the oil-containing milk is directed to a homogenizer, whereby the oildroplets are reduced in size and homogenously dispersed in the milk,following a mild homogenization at 10 bar. Then, the resultingoil-containing milk is held at 72° C. for 15 sec, cooled down to 4-6° C.and stored. Following cooling, a primary ingredient or a mixture thereofis added and mixed therein. The primary ingredient is preferablyselected from the group comprising sweeteners, stabilizers andthickeners. Examples of sweeteners include sucrose, fructose, glucose,aspartame, sorbitol, etc. Appropriate stabilizers and thickenersinclude, for example, carrageenan, sodium alginate, etc. The procedurefollows with the admixture of a secondary ingredient or a mixturethereof. The secondary ingredient for the making of an alternativecustard is preferably selected from the group comprising starch,modified starch, wheat semolina, etc. The quantities of the primary andsecondary ingredients used depend on the type of final milk-basedproduct and are in accordance with supplier specifications andregulation. Aromas (i.e. artificial and/or natural food grade, such asvanillin, strawberry extracts, etc.) and colourings (i.e. artificialand/or natural food grade, such as cochineal, beta-carotene, annatto,etc.) and optionally chocolate, nuts, etc may be added at this step,according to regulation and supplier specifications. Heat treatmentunder continuous stirring is then carried out at 90° C., for theingredients to be properly dissolved. The mixture is cooled to 70° C.before packaging. Finally, the packaged product is stored at 4° C.

The term “oil” is used as defined above.

The milk used for the preparation of the milk-based alternative productmay be whole milk or partially or wholly skimmed milk. The vegetable oilmay be used at least in partial substitution of milk fat. Milk can be ofcow, goat, sheep or buffalo origin, or any combination thereof.Stabilising agents or/and emulsifying agents may be used, if necessary,and according to the each intended product type.

In a preferred embodiment, inserting the oil in step c) is performed byan insertion tube with a diameter of about 32 mm.

In a further preferred embodiment the flow rate of the edible oil instep c) is about 1000 to 2000 liters/h, preferably 1000 liters/h, morepreferably 1500 liters/h and most preferably about 2000 liters/h.

In another embodiment the homogenization in step d) uses a two-stagehomogenizer with a piston diameter of about 55 mm.

The amount of the oil that is to be used for the preparation of theoil-containing milk-based products particularly depends on the kind ofoil, the kind of milk and the intended oil end concentration of themilk-based alternative products to be prepared.

An exemplary amount of the oil concentration of the mixture in step f)is between about 5 to 30 (w/w) %, more preferably 5 to 25 (w/w) % andeven more preferably about 5 to 20 (w/w) %.

According to the present invention, the oil-containing milk-basedproduct contains the oil as a substitute for the milk fat content. Themilk-based alternative product may, however, also contain both vegetableoil and milk fat.

A further object of the present invention is a milk-based alternativeproduct, in particular an ice cream alternative product, a custardalternative product or a chilled or frozen dessert alternative product,obtainable by a method comprising the steps of:

-   -   a) providing edible oil at a temperature of about 50 to 55° C.,    -   b) providing milk at about 2.3 bar, with a flow rate of about 10        to 12 tons/h, at about 55° C.,    -   c) inserting the oil at about 2.5 bar, with a flow rate of about        500 to 2000 liters/h, into the milk, to obtain a mixture,    -   d) subjecting the mixture to mild homogenization at about 10        bar,    -   e) pasteurizing the homogenized mixture at about 72° C. for        about 15 sec,    -   f) cooling the pasteurized mixture to about 4 to 6° C.,    -   g) further processing of the pasteurized mixture in order to        obtain a milk- based product, such as an ice cream, a custard, a        chilled or frozen dessert, using appropriate methodologies known        in the art suited for each product type,        wherein a milk-based alternative product is obtained, which        contains 5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat,        more preferably about 5 to 25 (w/w) % fat and most preferably        about 5 to 20 (w/w) % fat.

Further disclosed is the use of an edible oil for the production of amilk-based alternative product, in particular an ice cream alternativeproduct, a custard alternative product or a chilled or frozen desertalternative product, wherein the milk-based alternative product contains5 (w/w) % fat, preferably about 5 to 30 (w/w) % fat, more preferablyabout 5 to 25 (w/w) % fat and even more preferably about 5 to 20 (w/w) %fat.

The invention will be further understood by the skilled person withrespect to the figure, which shows a flow diagram of the inventiveprocess, and the examples. In particular, the flow diagram in FIG. 1shows the production of vegetable oil-containing milk based products.

EXAMPLES Example 1 An Exemplary Method For The Making Of A Semi-HardCheese Alternative Of Pasta Fillata Type.

Raw milk of <4° C., was preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour.

Next, the oil-containing skimmed milk with a preferred ratio offat/protein: 0.8-0.9 is directed along a tube to a homogenizer, whereinis subjected to mild homogenization. For example, homogenization may beperformed using a conventional two-stage homogenizer (Piston diameter 55mm) at 10 bar. The homogenized oil-containing milk mixture ispasteurized at 72° C. for 15 sec, and then cooled to 4-6° C. Theresulting oil-containing milk mixture is preheated up to 34-36° C., theninoculated with mesophilic and/or thermophilic starter culture andrennet (90% chymosin-10% pepsin) and left under conditions of 34-36° C.for 35-45 minutes, to acidify and coagulate. The curd is then cut intograins of <2-5 mm size, while being stirred, to commence syneresis.Following cutting of the curd, syneresis is further promoted by a heattreatment of two stages, wherein a temperature range of 48-51° C. isapplied. The heat treatment follows two successive “stirring & heating”stages, whereby the temperature is gradually increased, the twosuccessive “stirring & heating” stages, comprising of: i) 12 min at <42°C., ii) 8 min at <51° C. Then, the curd is subjected into a finalstirring stage of a duration of <45 min, whereby the temperature of thecurd is kept at <51° C. and a final pH value of 6.25 is obtained.

The residual whey is removed from the curd, using various ways known ina person of ordinary skill, depending on the intended type of cheese.For the making of semi-hard cheese alternatives, including of pastafillata type, pressing is adopted for a duration of 40 min, underconditions of 80-100 psi.

Then, the common cheese processing steps follow, using the conditionssuited for the preparation of semi-hard cheese product of pasta fillatatype, known in a person of ordinary skill.

Example 2 An Exemplary Method For The Making Of A Semi-Hard CheeseAlternative Of Pasta Fillata Type, Having Reduced Fat.

Raw milk of <4° C., was preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 fat vol-% skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour. Next, theoil-containing skimmed milk with a preferred ratio of fat/protein:0.4-0.5 is directed along a tube to a homogenizer, wherein is subjectedto mild homogenization. For example, homogenization may be performedusing a conventional two-stage homogenizer (Piston diameter 55 mm) at 10bar. The homogenized oil-containing milk mixture is pasteurized at72-74° C. for 15 sec and then cooled to 4-6° C. The resultingoil-containing milk mixture is preheated up to 34-36° C., inoculatedwith a suitable amount of mesophilic-thermophilic starter culture andrennet, comprising 90% chymosin-10% pepsin and left under conditions of34-36° C. for 35-45 minutes, to acidify and coagulate. The curd is thencut into grains of <2-5 mm size, while being stirred, to commencesyneresis. Following cutting of the curd, syneresis is further promotedby a heat treatment of two stages, wherein a temperature range of 38-48°C. is applied. The heat treatment follows two successive “stirring &heating” stages, whereby the temperature is gradually increased, the twosuccessive “stirring & heating” stages, comprising of: i) 8 min at <38°C., ii) 15 min at <48° C. Then, the curd is subjected into a finalstirring stage of a duration of <35 min, whereby the temperature of thecurd is kept at <48° C., and a final pH value of 6.2 is obtained.

The residual whey is removed from the curd, using various ways known ina person of ordinary skill, depending on the intended type of cheese.For the making of semi-hard cheese alternatives, including of pastafillata type, pressing is adopted for a duration of 40 min, underconditions of 80-100 psi.

The resulting product is further processed using conventional processingsteps, suited for the preparation of semi-hard cheese product of pastafillata type, known by a person of ordinary skill.

Example 3 An Exemplary Method For The Making Of A White CheeseAlternative In Brine.

a) Raw milk of <4° C., was preheated up to <55° C. Then, the preheatedmilk is introduced into a centrifugal separator, resulting in 50 vol-%fat cream and 0.03 vol-% skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour.

Next, the oil-containing skimmed milk with a preferred ratio offat/protein: 0.8-0.9 is directed along a tube to a homogenizer, whereinis subjected to mild homogenization. For example, homogenization may beperformed using a conventional two-stage homogenizer (Piston diameter 55mm) at 10 bar. The homogenized oil-containing milk mixture ispasteurized at 72° C. for 15 sec and then cooled to 4-6° C. Theresulting oil-containing milk mixture is preheated up to 36-38° C., theninoculated with a suitable amount bulk starter culture and rennet (90%chymosin-10% pepsin) and left under conditions of 36-38° C. for 50minutes to acidify and coagulate. The curd is then cut into cubes of <1cm×1 cm×2 cm or 2 cm×2 cm×2 cm in size, depending on the milk origin,i.e. from cow or sheep, respectively, to commence syneresis. Then, thecurd is left at rest for a period of 30-65 min, depending on the milkorigin, while the whey is separated from the curd. Afterwards, thebiggest volume of whey is removed and the curd is added to molds wherenatural drainage occurs.

The resulting product is further processed using conventional processingsteps, suited for the preparation of white cheese in brine, known by aperson of ordinary skill.

b) Raw milk of <4° C., was preheated up to <55° C. Then, the preheatedmilk is introduced into a centrifugal separator, resulting in 50 vol-%fat cream and 0.03 vol-% skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour.

Next, the oil-containing skimmed milk with a preferred ratio offat/protein: 0.8-0.9 is directed along a tube to a homogenizer, whereinis subjected to mild homogenization. For example, homogenization may beperformed using a conventional two-stage homogenizer (Piston diameter 55mm) at 10 bar. The homogenized oil-containing milk mixture ispasteurized at 72° C. for 15 sec and then cooled to 4-6° C. Theresulting oil-containing milk mixture is preheated up to 34-36° C., theninoculated with a suitable amount bulk starter culture and rennet (90%chymosin-10% pepsin) and left under conditions of 34-36° C. for 50minutes to acidify and coagulate. The curd is then cut into cubes of <1cm×1 cm×2 cm or 2 cm×2 cm×2 cm in size, depending on the milk origin,i.e. from cow or sheep, respectively, to commence syneresis. Then, thecurd is left at rest for a period of 30-65 min, depending on the milkorigin, while the whey is separated from the curd. Afterwards, thebiggest volume of whey is removed and the curd is added to molds wherenatural drainage occurs.

The resulting product is further processed using conventional processingsteps, suited for the preparation of white cheese in brine, known by aperson of ordinary skill.

Example 4

An Exemplary Method For The Making Of A Type Of White Cheese AlternativeIn Brine, Having Reduced Fat a) Raw milk of <4° C., was preheated up to<55° C. Then, the preheated milk is introduced into a centrifugalseparator, resulting in 50 vol-% fat cream and 0.03 vol-% fat skimmedmilk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour.

Next, the oil-containing skimmed milk with a preferred ratio offat/protein: 0.4-0.5 is directed along a tube to a homogenizer, whereinis subjected to mild homogenization. For example, homogenization may beperformed using a conventional two-stage homogenizer (Piston diameter 55mm) at 10 bar. The homogenized oil-containing milk mixture ispasteurized at 72° C. for 15 sec and then cooled to 4-6° C. Theresulting oil-containing milk mixture is preheated up to 35-36° C., theninoculated with a suitable amount of bulk starter culture and rennet(90% chymosin-10% pepsin) and left under conditions of 35-36° C. for 50minutes, to acidify and coagulate. The curd is then cut into cubes of <1cm×1 cm×2 cm or 2 cm×2 cm×2 cm in size, depending on the milk origin,i.e. from cow or sheep, respectively, to commence syneresis. Then, thecurd is left at rest for a period of 30-35 min, while the whey isseparated from the curd. Afterwards, the biggest volume of whey isremoved and the curd is added to molds, where natural drainage occurs.

The resulting product is further processed using conventional processingsteps, suited for the preparation of white cheese in brine, known by aperson of ordinary skill.

b) Raw milk of <4° C., was preheated up to <55° C. Then, the preheatedmilk is introduced into a centrifugal separator, resulting in 50 vol-%fat cream and 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour.

Next, the oil-containing skimmed milk with a preferred ratio offat/protein: 0.4-0.5 is directed along a tube to a homogenizer, whereinis subjected to mild homogenization. For example, homogenization may beperformed using a conventional two-stage homogenizer (Piston diameter 55mm) at 10 bar. The homogenized oil-containing milk mixture ispasteurized at 72° C. for 15 sec and then cooled to 4-6° C. Theresulting oil-containing milk mixture is preheated up to 34-36° C., theninoculated with a suitable amount of bulk starter culture and rennet(90% chymosin-10% pepsin) and left under conditions of 34-36° C. for 50minutes, to acidify and coagulate. The curd is then cut into cubes of <1cm×1 cm×2 cm or 2 cm×2 cm×2 cm in size, depending on the milk origin,i.e. from cow or sheep, respectively, to commence syneresis. Then, thecurd is left at rest for a period of 30-35 min, while the whey isseparated from the curd. Afterwards, the biggest volume of whey isremoved and the curd is added to molds, where natural drainage occurs.

The resulting product is further processed using conventional processingsteps, suited for the preparation of white cheese in brine, known by aperson of ordinary skill.

Example 5 An Exemplary Method For The Making Of Another Type OfSemi-Hard Cheese Alternative, Having Reduced Fat.

Raw milk of <4° C., was preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 vol-% fat skimmed whey.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a pressure of 2.5 bars and a flow rate of approximately1000-2000 liters per hour, preferably at >1500 liters per hour and evenmore preferably at 2000 liters per hour, via an insertion system ofdiameter 32 mm. The skimmed milk passes at a pressure of approximately2.3 bars and a flow rate at 10 tons/hour-12 tons/hour.

Next, the oil-containing skimmed milk is directed along a tube to ahomogenizer, wherein is subjected to mild homogenization. For example,homogenization may be performed using a conventional two-stagehomogenizer (Piston diameter 55 mm) at 10 bar. The homogenizedoil-containing milk mixture is pasteurized at 72° C. for 15 sec, andthen cooled to 4-6° C. The resulting oil-containing milk mixture with apreferred ratio of fat/protein: 0.4-0.5 is preheated up to 31-32° C.,then inoculated with a suitable mesophilic-thermophilic starter cultureand rennet comprising of 90% chymosin-10% pepsin and left underconditions of 31-32° C. for 35-45 minutes, to acidify and coagulate. Thecurd is then cut into grains of <2-5 mm size, while being stirred, tocommence syneresis. Following cutting of the curd, the whey is drainedfrom the tank in a proportion of 40%. Then, 35% of warm water in 36° C.is added and a heat treatment follows, under stirring, wherein atemperature range of 34° C. is applied for 40 min and a final pH valueof 5.4-5.6 is obtained. For the making of this type of semi-hard cheesealternative, pressing is adopted for a duration of 40 min, underconditions of 80-100 psi.

The resulting product is further processed using conventional processingsteps, suited for the preparation of a semi-hard cheese product, knownby a person of ordinary skill.

Example 6 An Exemplary Method For The Making Of A Whey CheeseAlternative.

Whey of <4° C., was preheated up to <55° C. Then, the pre-heated whey isintroduced into a centrifugal separator, resulting in 50 vol-% fat creamand 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed whey at a flow rate 1000-2000 liters per hour, preferablyat >1500 liters per hour and even more preferably at 2000 liters perhour, via an insertion system of diameter 32 mm, fitted in closeproximity and parallel configuration to the entrance system of fat creamre-feeding. Next, the oil-containing skimmed whey is directed along atube to a homogenizer, wherein is subjected to homogenization, at 120bar. Homogenization may be performed using a conventional two-stagehomogenizer (Piston diameter 55 mm). The homogenized oil-containing wheymixture is subjected to a heat treatment, applying a graduallyincreasing temperature up to 96° C. At the temperature of −60° C. (<65°C.), 9% skimmed milk is added and the heat treatment continues until thetemperature of 96° C. is reached. The resulting product is then left atrest at the temperature of 96° C. for 20-30 minutes. By that time, thecoagulum is found to float on the surface of the extracted whey. Then,the whey is drained off, while the coagulum is transferred to conditionsof 4° C.

Example 7 An Exemplary Method For The Making Of A Hard CheeseAlternative.

Raw milk of <4° C., was preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed whey at a flow rate 1000-2000 liters per hour, preferablyat >1500 liters per hour and even more preferably at 2000 liters perhour, via an insertion system of diameter 32 mm, fitted in closeproximity and parallel configuration to the entrance system of fat creamre-feeding.

Next, the oil-containing skimmed milk is directed along a tube to ahomogenizer, wherein is subjected to mild homogenization. For example,homogenization may be performed using a conventional two-stagehomogenizer (Piston diameter 55 mm) at 10=bar. The homogenizedoil-containing milk mixture is pasteurized at 72° C. for 15 sec and thencooled to 4-6° C. The resulting oil-containing milk mixture with apreferred ratio of fat/protein: 1.0-1.1 is preheated up to 34-36° C.,inoculated with a suitable mix of mesophilic-thermophilic-propionic acidstarter culture and rennet (90% chymosin-10% pepsin) and left tocoagulate under conditions of 34-36° C. for 35 minutes. The curd, isthen cut into grains of <5-8 mm size, while being stirred, to commencesyneresis. To promote syneresis, the coagulum is heated to the range48-49° C. for 8 minutes, while stirred. During this step of heattreatment and while temperature reaches the 46° C., an amount of 20% ofwhey is replaced by an equal amount of water. The water added is of 45°C. The heat treatment continues, under stirring, until the temperatureof the mixture reaches the 48.5° C. At this temperature, the mixturecomprising curd, water and whey, is left to rest for 10 minutes.Pressing (at 80-100 psi) is then applied to drain the remaining whey andwater off the curd. The pH of the curd, following pressing, is of therange of 5.3-5.4.

The resulting product is further processed using conventional processingsteps, suited for the preparation of a hard cheese product, known by aperson of ordinary skill.

Example 8 An Exemplary Method For The Making Of A Soft Spreadable CheeseAlternative.

Raw milk of <4° C., was preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a flow rate 2000 liters per hour, via an insertionsystem of diameter 32 mm, fitted in close proximity and parallelconfiguration to the entrance system of fat cream re-feeding. Next, theoil-containing skimmed milk is directed along a tube to a homogenizer,wherein is subjected to mild homogenization at 10 bar. For example,homogenization may be performed using a conventional two-stagehomogenizer (Piston diameter 55 mm) at 10 bar. The homogenizedoil-containing milk mixture is pasteurized at 72° C. for 15 sec, andthen cooled to 4-6° C. The resulting oil-containing milk mixture with apreferred ratio of fat/protein: 1:1.1 is preheated up to 25-30° C. andinoculated with a suitable mesophilic-thermophilic starter culture,until the pH reaches 6.2. Then, the appropriate amount of rennet (50%chymosin-50% pepsin) is added therein, for the coagulation to becompleted after 12 hours. The curd is then cut into cubes of 2 cm×2 cm×2cm and left at rest for 4-5 hours. The curd is then drained and salted(−2%) and finally molded. The smooth cheese is then stored at 4° C.

Example 9 An Exemplary Method For The Making Of An Ice Cream AlternativeProduct.

Raw milk of <4° C., is preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a flow rate of 1000-2000 liters/hour, preferably at arate greater than 1500 liters/hour and even more preferably at 2000liters/hour, via an insertion system of diameter 32 mm, fitted in closeproximity and parallel configuration to the entrance system of fat creamre-feeding.

Next, the oil-containing skimmed milk is directed along a tube to ahomogenizer, where it is subjected to a mild homogenization. Forexample, the homogenization may be performed using a conventionaltwo-stage homogenizer Piston diameter (55 mm) at 10 bar. The homogenizedoil-containing milk mixture is subjected to pasteurisation (72° C. for15 sec) and then cooled to 4-6° C. Appropriate amounts of sucrose(5.0-10.0 g/kg), glucose (5.0-10.0 g/kg) and carrageenan (5.0-10.0 g/kg)are then added thereto and mixed. The procedure follows with theoptional addition of 100-200 g/kg of milk cream and 1-3 g/kg ofglycerine monostearate and further mixing. The resulting mixture is thensubjected to a heat treatment until a temperature of 68° C. has beenreached and homogenization at 100 bar. The homogenized mixture is thenpasteurized (78-80° C. for 20 to 25 seconds) and left to cool to 5° C.Incubation is performed at 5° C. for at least 4 hours to set the mixtureand ensure an optimal “body” in the end product. Following the previousincubation step, the mixture is subjected to freezing and whipping(“churning”) at −6° C. in order to develop the favourable ice crystalsize and to incorporate a desirable amount of air (“overrun”). Additionof aromas (such as vanillin) and colourings (such as annatto) may beadded according to regulation and supplier specification. Then, themixture is filled and frozen at −40° C. (by a blast freezer), beforestorage at −20° C.

Example 10

An Exemplary Method For The Making Of A Caramel Custard (Crème Caramel)Alternative Product.

Raw milk of <4° C., was preheated up to <55° C. Then, the preheated milkis introduced into a centrifugal separator, resulting in 50 vol-% fatcream and 0.03 vol-% fat skimmed milk.

Vegetable oil is preheated to 55° C. and then introduced into theskimmed milk at a flow rate 1000-2000 liters/hour, preferably at a rategreater than 1500 liters/hour and even more preferably at 2000liters/hour, via an insertion system of diameter 32 mm, fitted in closeproximity and parallel configuration to the entrance system of fat creamre-feeding.

Next, the oil-containing skimmed milk is directed along a tube to ahomogenizer, where it is subjected to a mild homogenization. Forexample, the homogenization may be performed using a conventionaltwo-stage homogenizer Piston diameter (55 mm) at 10 bar. The homogenizedoil-containing milk mixture is pasteurized at 72° C. for 15 sec and thencooled to 4-6° C. Following cooling, the following ingredients aresuccessively added and mixed therein: sucrose (90 g/kg) and optionallymilk cream (40 g/kg). The procedure follows with the admixture of a mixof carrageenan and starches (e.g. tapioca starch, wheat starch and wheatsemolina) 60 g/kg and further mixing. Then, 0.5 g/kg of vanillin and areadded. For all the ingredients to be properly dissolved, a heattreatment step follows (90° C. for up to 30 min). The mixture is cooledto 70° C. before packaging. For caramel custard making, the packagingcontainer is filled with a layer of caramel, prior to addition of theabove milk-based mixture. Finally, the packaged dessert is stored at 4°C.

1. A method for producing a cheese alternative product comprising thesteps of: a) providing edible oil at a temperature of about 50 to 55°C., b) providing milk at about 2.3 bar, with a flow rate of about 10 to12 tons/h, at about 55, c) inserting the oil at about 2.5 bar, with aflow rate of about 500 to 2000 liters/h, into the milk, to obtain amixture, d) subjecting the mixture to mild homogenization at about 10bar, e) pasteurizing the homogenized mixture at about 72° C. for about15 sec, f) cooling the pasteurized mixture to about 4 to 6° C., g)subjecting the mixture to a curd formation, h) performing a curd andwhey separation, wherein a cheese alternative product is obtained, whichcontains ≧5 (w/w) % fat.
 2. The method of claim 1, wherein the milk iswhole milk, semi-skimmed milk or skimmed milk.
 3. The method of claim 2,wherein inserting the oil in step c) is performed by an insertion tubewith a diameter of about 30-40 mm.
 4. The method of claim 3, wherein theflow rate of the edible oil in step c) is about 500 to 2000 liters/h. 5.The method of claim 4, wherein the homogenization in step d) uses atwo-stage homogenizer with a piston diameter of about 55 mm.
 6. Themethod of claim 5, wherein the mixture in step f) comprises edible oilat a concentration of about 4 to 17 (w/w) %.
 7. The method of claim 6,wherein the fat is a mixture of milk fat and edible oil.
 8. A cheesealternative product obtainable by a method comprising the steps of a)providing edible oil at a temperature of about 50 to 55° C., b)providing milk at about 2.3 bar, with a flow rate of about 10 to 12tons/h, at about 55° C., c) inserting the oil at about 2.5 bar, with aflow rate of about 500 to 2000 liters/h, into the milk, to obtain amixture, d) subjecting the mixture to mild homogenization at about 10bar, e) pasteurizing the homogenized mixture at about 72° C. for about15 sec, f) cooling the pasteurized mixture to about 4 to 6° C., g)subjecting the mixture to a curd formation, h) performing a curd andwhey separation, wherein a cheese alternative product is obtained, whichcontains >5 (w/w) % fat. 9-18. (canceled)
 19. The method of claim 1,wherein the cheese alternative product is obtained, which contains 5 to30 (w/w) % fat.
 20. The method of claim 1, wherein the cheesealternative product is obtained, which contains 5 to 25 (w/w) % fat. 21.The method of claim 1, wherein the cheese alternative product isobtained, which contains 5 to 20 (w/w) % fat.
 22. The method of claim 2,wherein the milk is skimmed milk.
 23. The method of claim 4, wherein theflow rate of the edible oil in step c) is about 1000 to 2000 liters/h.24. The method of claim 4, wherein the flow rate of the edible oil instep c) is about 1500 to 2000 liters/h.
 25. The method of claim 4,wherein the flow rate of the edible oil in step c) is about 2000liters/h.
 26. The method of claim 6, wherein the mixture in step f)comprises edible oil at a concentration of about 8 to 17 (w/w) %. 27.The method of claim 6, wherein the mixture in step f) comprises edibleoil at a concentration of about 9 to 17 (w/w) %.
 28. The method of claim7, wherein the fat is vegetable oil.
 29. The method of claim 7, whereinthe fat is olive oil.
 30. The method of claim 8, wherein the cheesealternative product is obtained, which contains 5 to 30 (w/w) % fat. 31.The method of claim 8, wherein the cheese alternative product isobtained, which contains 5 to 25 (w/w) % fat.
 32. The method of claim 8,wherein the cheese alternative product is obtained, which contains 5 to20 (w/w) % fat.